The activities of hydrogenase and enoate reductase in two Clostridium species,their interrelationship and dependence on growth conditions

The enzyme activities of Clostridium La 1 and Clostridium kluyveri involved in the stereospecific hydrogenation of ,-unsaturated carbonyl compounds with hydrogen gas were measured. In C. La 1 the specific activities of hydrogenase and enoate reductase depended heavily on the growth phase and the composition of the medium. During growth in batch cultures on 70 mM crotonate the specific activity of hydrogenase increased and then dropped to about 10% of its maximum value, whereas the activity of enoate reductase reached its maximum in cells of the stationary phase. Under certain conditions during growth the activity ratio hydrogenase: enoate reductase changed from 120 to 1. Thus, the rate limiting enzyme for the hydrogenation can be either the hydrogenase or the enoate reductase, depending on the growth conditions of the cells.The specific activities of ferredoxin-NAD reductase and butyryl-CoA dehydrogenase increased 3-4-fold during growth on crotonate. By turbidostatic experiments it was shown that at constant input of high crotonate concentrations (200 mM) the enoate reductase activity was almost completely suppressed; it increased steadily with decreasing crotonate down to an input concentration of 35 mM.Glucose as carbon source led to high hydrogenase and negligible enoate reductase activities. The latter could be induced by changing the carbon source of the medium from glucose to crotonate. Tetracycline inhibited the formation of enoate reductase.A series of other carbon sources was tested. They can be divided into ones which result in high hydrogenase and rather low enoate reductase activities and others which cause the reverse effect.When the Fe²⁺ concentration in crotonate medium was growth limiting, cells with relatively high hydrogenase activity and very low enoate reductase activity in the stationary phase were obtained. At Fe²⁺ concentrations above 3·10^-7 M enoate reductase increased and hydrogenase activity reached its minimum. The ratio of activities changes by a factor of about 200. In a similar way the dependence of enzyme activities on the concentration of sulfate was studied.In batch cultures of Clostridium kluyveri a similar opposite time course of enoate reductase and hydrogenase was found.The possible physiological significance of this behavior is discussed.Non Standard Abbreviations O.D.₅₇₈ Optical density at 578 nm Dedicated to Professor Dr. O. Kandler on the occasion of his 60th birthday     

Characterization of catalytic properties of hydrogenase isolated from the unicellular cyanobacterium Gloeocapsa alpicola CALU 743

The main catalytic properties of the Hox type hydrogenase isolated from the Gloeocapsa alpicola cells have been studied. The enzyme effectively catalyzes reactions of oxidation and evolution of H2 in the presence of methyl viologen (MV) and benzyl viologen (BV). The rates of these reactions in the interaction with the physiological electron donor/acceptor NADH/NAD+ are only 3-8% of the MV(BV)-dependent values. The enzyme interacts with NADP+ and NADPH, but is more specific to NAD+ and NADH. Purification of the hydrogenase was accompanied by destruction of its multimeric structure and the loss of ability to interact with pyridine nucleotides with retained activity of the hydrogenase component (HoxYH). To show the catalytic activity, the enzyme requires reductive activation, which occurs in the presence of H2, and NADH accelerates this process. The final hydrogenase activity depends on the redox potential of the activation medium (E(h)). At pH 7.0, the enzyme activity in the MV-dependent oxidation of H2 increased with a decrease in E(h) from -350 mV and reached the maximum at E(h) of about -390 mV. However, the rate of H2 oxidation in the presence of NAD+ in the E(h) range under study was virtually constant and equal to 7-8% of the maximal rate of H2 oxidation in the presence of MV.     

Effect of redox potential on activity of hydrogenase 1 and hydrogenase 2 in Escherichia coli

This report elucidates the distinctions of redox properties between two uptake hydrogenases in Escherichia coli. Hydrogen uptake in the presence of mediators with different redox potential was studied in cell-free extracts of E. coli mutants HDK103 and HDK203 synthesizing hydrogenase 2 or hydrogenase 1, respectively. Both hydrogenases mediated H(2) uptake in the presence of high-potential acceptors (ferricyanide and phenazine methosulfate). H(2) uptake in the presence of low-potential acceptors (methyl and benzyl viologen) was mediated mainly by hydrogenase 2. To explore the dependence of hydrogen consumption on redox potential of media in cell-free extracts, a chamber with hydrogen and redox ( E(h)) electrodes was used. The mutants HDK103 and HDK203 exhibited significant distinctions in their redox behavior. During the redox titration, maximal hydrogenase 2 activity was observed at the E(h) below -80 mV. Hydrogenase 1 had maximum activity in the E(h) range from +30 mV to +110 mV. Unlike hydrogenase 2, the activated hydrogenase 1 retained activity after a fast shift of redox potential up to +500 mV by ferricyanide titration and was more tolerant to O(2). Thus, two hydrogenases in E. coli are complementary in their redox properties, hydrogenase 1 functioning at higher redox potentials and/or at higher O(2) concentrations than hydrogenase 2.     

Cultivation of Methylosinus trichosporium OB3b: III. production of particulate methane monooxygenase in continuous culture

Continous culture experiments with the obligatory methanotroph, Methylosinus trichosporium OB3b, were conducted to study the whole-cell methane monooxygenase (MMO) and nitrogenase activities in a nitrate minimal salts medium under oxygen-limited conditions with methane as the carbone source. The important variables investigated were the feed medium concentrations of copper and nitrate, CO(2) addition, the agitation speed, and the dilution rate. M. trichosporium OB3b required quantitative amounts of copper (2.6 x 10(-4) g Cu/g dry cell Wt) for the exclusive production of particulate MMo during continous culture growth. When the feed medium nitrate concentration was varied in the range of 5-50 mM, the whole-cell specific pMMO activity exhibited a maximum at 40 mM. The elimination of external CO(2) gassing decreased pMMO activity by more than 30%. The steady-state cell density increased continuously over a 300-700 rpm range of agitation speed, whereas, the pMMO activity became maximal at 400 rpm. Also, the pMMO activity increased with the dilution rate up to 0.06 h(-1) and remained constant thereafter. Maximal continuous pMMO productivity was, thus, achieved in Higgin's medium containing 10 muM Cu, 80 muM Fe, and 40 mM nitrate with an agitation speed of 500 rpm and a dilution rate of 0.06 h(-1). Nitrogenase activity, on the other hand, increased over a feed medium copper concentration of 2-15 muM, falling sharply at 20 muM, and it exhibited a minimum at 20 mM when the feed medium nitrate concentration was varied. (c) 1992 John Wiley & Sons, Inc.     

Metabolic characterization of a L-lysine-producing strain by continuous culture

Continuous culture experiments with the L-producer, Corynebacterium glutamicum, were carried out to characterize the effect of specific growth rate on fermentation yields, specific rates, productivities, and fluxes through the primary metabolism. The specific productivity of L-lysine exhibited a maximum with respect to specific growth rate, with an initial growth-associated behavior up to specific growth rates of about 0.1 h(-1), and a constant specific productivity for specific growth rates in the range of about 0.1 to 0.2 h(-1). The productivity dropped at specific growth rates larger than about 0.2 h(-1). The yield of L-lysine on glucose increased approximately linearly with decreasing specific growth rate over the entire range studied, as did the respiratory quotient. A direct relationship was established between the culture respiratory quotient and the L-lysine yield. By explicitly accounting for glucose used for biomass synthesis, it was shown that the strain synthesizes L-lysine with an intrinsic yield, or efficiency, of about 0.41 mol L-lysine/mol glucose, compared with the theoretical yield of 0.75 mol/mol. Metabolic flux modeling based on the continuous culture data suggests that the production of ATP is not likely to be a limiting factor in L-lysine production, and that a high TCA cycle activity, coupled with a tightly controlled split of metabolite flow at the PEP node, is likely the cause of the large discrepancy between theoretical and actual yields in L-lysine fermentations.     

Improved production of recombinant ovine interferon-tau by mut(+) strain of Pichia pastoris using an optimized methanol feed profile

Recombinant ovine interferon-tau (r-oIFN-tau) production by Pichia pastoris was studied using methanol as the sole carbon source during induction. The cells were grown on glycerol up to a certain cell density before induction of the AOX1 promoter by methanol for expression of the recombinant protein. Cell growth on methanol has been modeled using a substrate-feed equation, which served as the basis for an effective computer control of the process. The r-oIFN-tau concentration in the culture began to decline despite continued cell growth after 50 (+/- 6) h of induction, which was associated with an increase in proteolytic activity of the fermentation broth. A specific growth rate of 0.025 h(-1) was found to be optimal for r-oIFN-tau production. No significant improvement in r-oIFN-tau production was observed when the specific growth rate was stepped up before the critical point when r-oIFN-tau concentration started decreasing during fermentation. However, best results were obtained when the specific growth rate was stepped down from 0.025 to 0.02 h(-1) at 38 h of induction, whereby the active production period was prolonged until 70 h of induction and the broth protease activity was correspondingly reduced. The corresponding maximum protein yield was 391.7 mg x L(-1) after 70 h of fermentation. The proteolytic activity could be reduced by performing fermentations at specific growth rates of 0.025 h(-1) or below. The recombinant protein production can be performed at an optimal yield by directly controlling the methanol feed rate by a computer-controlled model. The production profile of r-oIFN-tau was found to be significantly different from other secreted and intracellular recombinant protein processes, which is an indication that recombinant protein production in Pichia pastoris needs to be optimized as individual processes following established principles.     

Continuous cultivation of recombinant Escherichia coli: Existence of an optimum dilution rate for maximum plasmid and gene product concentration

Growth yield factors, plasmid stability, cellular plasmid content, and cloned gene product activity for Escherichia coli HB101 containing plasmid pDM246 were measured at several dilution rates in continuous culture. Cell mass yield per mass of glucose consumed declined with increasing dilution rate. There was no evidence of plasmid segregational instability in any experiments, none of which employed selective medium. Plasmid content per cell varied with population-specific growth rate as observed in earlier batch experiments with the same strain. Plasmid content declined with increasing specific growth rate following indication of a maximum number of plasmids per cell at specific growth rates of ca. 0.3 h(-1). Cloned gene product (beta-lactamase) activity exhibited a sharp maximum with respect to dilution rate in continuous culture. Qualitatively different results were observed in previous experiments in batch cultivation in which specific growth rate changes were effected by altering medium composition.     

Physiology of nitrogen fixation in Azospirillum lipoferum Br 17 (ATCC 29 709)

Changes of cellular activities during batch cultures with Azospirillum lipoferum strain Br 17 (ATCC 29 709) were observed within the growth cycle, at optimal pO₂ (0.002–0.003 atm). The relative growth rate for cells growing with N₂ as sole nitrogen source during log phase was =0.13 h^-1 and the doubling time was 5.3 h. Nitrogenase activity was not accompanied by hydrogen evolution at any growth stage, and a very active uptake hydrogenase was demonstrated. The hydrogenase activity increased towards the end of the growth period when glucose became limiting and N₂ fixation reached its maximal specific activity. Oxygen consumption and oxygen tolerance at the various growth stages, increased simultaneously with the uptake hydrogenase activity indicating a possible role of this enzyme in an oxygen protection mechanism of A. lipoferum nitrogenase. The efficiency of nitrogen fixation expressed as mg total nitrogen fixed in cells and supernatant per g glucose consumed, was 20 at the early log phase and increased to 48 at the late log phase. About 25% of the total fixed nitrogen was recovered in the culture supernatant.Abbreviations DOT Dissolved oxygen tension - PHB Poly--hydroxybutyric acid - O.D. Optical density (560 nm) - A.T.C.C. American type culture collection - NTA Nitrilotriacetic acid Graduate student of the Universidade Federal Rural do Rio de Janeiro, Brazil     

Improved production of live cells of Lactobacillus rhamnosus by continuous cultivation using glucose-yeast extract medium

In this study, the growth kinetics of Lactobacillus rhamnosus and lactic acid production in continuous culture were assessed at a range of dilution rates (0.05 h(-1) to 0.40 h(-1)) using a 2 L stirred tank fermenter with a working volume of 600 ml. Unstructured models, predicated on the Monod and Luedeking-Piret equations, were employed to simulate the growth of the bacterium, glucose consumption, and lactic acid production at different dilution rates in continuous cultures. The maximum specific growth rate of L. rhamnosus, mu-max, was estimated at 0.40 h(-1), and the Monod cell growth saturation constant, Ks, at approximately 0.25 g/L. Maximum cell viability (1.3 x 10(10) CFU/ml) was achieved in the dilution rate range of D = 0.28 h(-1) to 0.35 h(-1). Both maximum viable cell yield and productivity were achieved at D = 0.35 h(-1). The continuous cultivation of L. rhamnosus at D = 0.35 h(-1) resulted in substantial improvements in cell productivity, of 267% (viable cell count) that achieved via batch cultivation.     

Regulation of formate dehydrogenase activity in Methanococcus thermolithotrophicus.

Methanococcus thermolithotrophicus can use either H2 or formate as the electron donor for methanogenesis from CO2. Resuspended-cell experiments revealed that the ability to use H2 as the source of electrons for methanogenesis was constitutive; cells grown on formate or H2-CO2 were equally capable of H2-CO2 methanogenesis. The ability to metabolize formate at high rates was observed only in cells previously grown on formate. Two such strains were distinguished: strain F and strain HF. Strain F was repeatedly grown exclusively on formate for over 3 years; this strain showed a constitutive capacity to metabolize formate to methane, even after subsequent repeated transfers to medium containing only H2-CO2. Strain HF could only metabolize formate to methane when grown in the presence of formate with no H2 present; this strain was recently derived from another strain (H) that had been exclusively grown on H2-CO2 and which upon initial transfer to formate medium could only metabolize formate to methane at a very slow rate. Initial adaptation of strain H to growth on formate was preceded by a long lag. The specific activities of hydrogenase and formate dehydrogenase in cell extracts derived from these different strains confirmed these findings. Similar levels of hydrogenase were observed in all strains, independent of the presence of H2 in the growth medium medium. High levels of formate dehydrogenase were also constitutive in strain F. Only low formate dehydrogenase activities were observed in strain H. High levels of formate dehydrogenase were observed in strain HF only when these cells were grown with formate in the absence of H2. In all strains the two- to threefold fluctuations of both hydrogenase and formate dehydrogenase cell-free activities were observed during growth, with peak activities reached in the middle of the exponential phase.     

Kinetic study and mathematical modeling of methanogenesis of acetate using pure cultures of methanogens

Kinetics of methanogenesis from acetate was studied using pure cultures of Methanosarcina barkeri and Methanosarcina mazei. Methane formation was found to be associated with cell growth. Nearly equimolar methane was produced from acetate during the methanogenic growth, and about 1.94 g of cells were formed from each mole of acetate consumed. Cell growth can be estimated from methane production. Significant substrate inhibition was found when acetate concentration was higher than 0.12 M. Among the three methanogenic strains studied, M. mazei strain S6 had the highest specific growth rate at all acetate concentrations studied and was least sensitive to environmental factors investigated (e.g., acetate concentration). The maximum specific growth rate found for strain S6 was 0.022 hr(-1) at acetic acid concentration around 7 g/L. The other two strains studied were M. barkeri strain 227 and strain MS. Growth of M. barkeri was completely inhibited at sodium acetate concentrations higher than 0.24 M. The maximum specific growth rate found for strains 227 and MS was 0.019 and 0.021 h(-1) at acetic acid concentrations of 3.6 and 6.8 g/L, respectively. A kinetic model with substrate inhibition was developed and can be used to simulate the methane formation from M. mazei strain S6 grown on acetate at 35 degrees C, pH 7.     

Modeling Pichia pastoris growth on methanol and optimizing the production of a recombinant protein, the heavy-chain fragment C of botulinum neurotoxin, serotype A

An unstructured growth model for the recombinant methylotrophic yeast P. pastoris Mut(+) expressing the heavy-chain fragment C of botulinum neurotoxin serotype A [BoNT/A(H(c))], was successfully established in quasi-steady state fed-batch fermentations with varying cell densities. The model describes the relationships between specific growth rate and methanol concentration, and the relationships between specific methanol and ammonium consumption rates and specific growth rate under methanol-limited growth conditions. The maximum specific growth rate (mu) determined from the model was 0.08 h(-1) at a methanol concentration of 3.65 g/L, while the actual maximum mu was 0.0709 h(-1). The maximum specific methanol consumption rate was 0.0682 g/g WCW/h. From the model, growth can be defined as either methanol-limited or methanol-inhibited and is delineated at a methanol concentration of 3.65 g/L. Under inhibited conditions, the observed biomass yield (Y(X/MeOH)) was lower and the maintenance coefficient (m(MeOH)) was higher than compared to limited methanol conditions. The Y(X/MeOH) decreased and m(MeOH) increased with increasing methanol concentration under methanol-inhibited conditions. BoNT/A(H(c)) content in cells (alpha) under inhibited growth was lower than that under limited growth, and decreased with increasing methanol concentration. A maximum alpha of 1.72 mg/g WCW was achieved at a mu of 0.0267 h(-1) and induction time of 12 h.     

Optimization of a two-stage recombinant fermentation process: the dilution rate effect

The effects of dilution rates on the performance of a two-stage fermentation system for a recombinant Escherichia coli culture were studied. Dilution rate determines the apparent or averaged specific growth rate of a heterogeneous population of cells in the recombinant culture. The specific growht rate affects the genetic parameters involved in product formation in the second stage, such as plasmid stability, plasmid content, and specific gene expression rate. Kinetic models and correlations were developed for these parameters based on experimental data. Simulations of plasmid stability in the first stage showed that for longer fermentation periods, plasmid stability is better at higher dilution rates. However, the plasmid content is lower at these dilution rates. The optimal apparent specific growth rate for maximum productivity in the second stage was determined using two methods: (1) direct search for a constant specific growth rate, and (2) dynamic optimization using the maximum principle for a time-dependent specific growth rate profile. The results of the calculations showed that the optimum constant apparent specific growth rate for maximum over-all productivity is 0.40 h(-1). This coincides with the optimal specific growht rate for maximum plasmid content in the expressed stage. A 3.5% increase in overall productivity can be obtained by using a linear time dependent apparent specific growth rate control, mu(2)(t) = 0.0007t, in the course of the fermentation time.     

Growth and population dynamics of anaerobic methane-oxidizing archaea and sulfate-reducing bacteria in a continuous-flow bioreactor

The consumption of methane in anoxic marine sediments is a biogeochemical phenomenon mediated by two archaeal groups (ANME-1 and ANME-2) that exist syntrophically with sulfate-reducing bacteria. These anaerobic methanotrophs have yet to be recovered in pure culture, and key aspects of their ecology and physiology remain poorly understood. To characterize the growth and physiology of these anaerobic methanotrophs and the syntrophic sulfate-reducing bacteria, we incubated marine sediments using an anoxic, continuous-flow bioreactor during two experiments at different advective porewater flow rates. We examined the growth kinetics of anaerobic methanotrophs and Desulfosarcina-like sulfate-reducing bacteria using quantitative PCR as a proxy for cell counts, and measured methane oxidation rates using membrane-inlet mass spectrometry. Our data show that the specific growth rates of ANME-1 and ANME-2 archaea differed in response to porewater flow rates. ANME-2 methanotrophs had the highest rates in lower-flow regimes (mu(ANME-2) = 0.167 . week(-1)), whereas ANME-1 methanotrophs had the highest rates in higher-flow regimes (mu(ANME-1) = 0.218 . week(-1)). In both incubations, Desulfosarcina-like sulfate-reducing bacterial growth rates were approximately 0.3 . week(-1), and their growth dynamics suggested that sulfate-reducing bacterial growth might be facilitated by, but not dependent upon, an established anaerobic methanotrophic population. ANME-1 growth rates corroborate field observations that ANME-1 archaea flourish in higher-flow regimes. Our growth and methane oxidation rates jointly demonstrate that anaerobic methanotrophs are capable of attaining substantial growth over a range of environmental conditions used in these experiments, including relatively low methane partial pressures.     

A rational approach to improving productivity in recombinant Pichia pastoris fermentation

A Mut(S) Pichia pastoris strain that had been genetically modified to produce and secrete sea raven antifreeze protein was used as a model system to demonstrate the implementation of a rational, model-based approach to improve process productivity. A set of glycerol/methanol mixed-feed continuous stirred-tank reactor (CSTR) experiments was performed at the 5-L scale to characterize the relationship between the specific growth rate and the cell yield on methanol, the specific methanol consumption rate, the specific recombinant protein formation rate, and the productivity based on secreted protein levels. The range of dilution rates studied was 0. 01 to 0.10 h(-1), and the residual methanol concentration was kept constant at approximately 2 g/L (below the inhibitory level). With the assumption that the cell yield on glycerol was constant, the cell yield on methanol increased from approximately 0.5 to 1.5 over the range studied. A maximum specific methanol consumption rate of 20 mg/g. h was achieved at a dilution rate of 0.06 h(-1). The specific product formation rate and the volumetric productivity based on product continued to increase over the range of dilution rates studied, and the maximum values were 0.06 mg/g. h and 1.7 mg/L. h, respectively. Therefore, no evidence of repression by glycerol was observed over this range, and operating at the highest dilution rate studied maximized productivity. Fed-batch mass balance equations, based on Monod-type kinetics and parameters derived from data collected during the CSTR work, were then used to predict cell growth and recombinant protein production and to develop an exponential feeding strategy using two carbon sources. Two exponential fed-batch fermentations were conducted according to the predicted feeding strategy at specific growth rates of 0.03 h(-1) and 0.07 h(-1) to verify the accuracy of the model. Cell growth was accurately predicted in both fed-batch runs; however, the model underestimated recombinant product concentration. The overall volumetric productivity of both runs was approximately 2.2 mg/L. h, representing a tenfold increase in the productivity compared with a heuristic feeding strategy.     

Selenium increases hydrogenase expression in autotrophically cultured Bradyrhizobium japonicum and is a constituent of the purified enzyme.

We have investigated the effect of added selenite on autotrophic growth and the time course of hydrogen oxidation derepression in Bradyrhizobium japonicum 122DES cultured in a medium purified to remove selenium compounds. In addition, hydrogenase was purified to near homogeneity and examined for the specific incorporation of Se into the enzyme. The addition of Se at 0.1 microM significantly increased total cell protein and hydrogenase specific activity of harvested cells. Also, the addition of SeO3(2-) enhanced the time course of hydrogenase derepression by 133%, whereas VO3, AsO2(2-), SO2(2-), and TeO3(2-) failed to substantially affect hydrogenase derepression. During the final chromatographic purification of hydrogenase, a striking coincidence in peaks of protein content, Se radioactivity, and hydrogenase activity of fractions was obtained. The total Se content expressed per milligram of protein increased manyfold during the purification procedure. The mean Se content of the purified hydrogenase was 0.56 +/- 0.13 mol of Se per mol of enzyme. These results indicate that Se is an important element in the H2 metabolism of B. japonicum and that hydrogenase from B. japonicum is a seleno protein.     

Purification and catalytic properties of Ech hydrogenase from Methanosarcina barkeri.

Methanosarcina barkeri has recently been shown to produce a multisubunit membrane-bound [NiFe] hydrogenase designated Ech (Escherichia coli hydrogenase 3) hydrogenase. In the present study Ech hydrogenase was purified to apparent homogeneity in a high yield. The enzyme preparation obtained only contained the six polypeptides which had previously been shown to be encoded by the ech operon. The purified enzyme was found to contain 0.9 mol of Ni, 11.3 mol of nonheme-iron and 10.8 mol of acid-labile sulfur per mol of enzyme. Using the purified enzyme the kinetic parameters were determined. The enzyme catalyzed the H2 dependent reduction of a M. barkeri 2[4Fe-4S] ferredoxin with a specific activity of 50 U x mg protein-1 at pH 7.0 and exhibited an apparent Km for the ferredoxin of 1 microM. The enzyme also catalyzed hydrogen formation with the reduced ferredoxin as electron donor at a rate of 90 U x mg protein-1 at pH 7.0. The apparent Km for the reduced ferredoxin was 7.5 microM. Reduction or oxidation of the ferredoxin proceeded at similar rates as the reduction or oxidation of oxidized or reduced methylviologen, respectively. The apparent Km for H2 was 5 microM. The kinetic data strongly indicate that the ferredoxin is the physiological electron donor or acceptor of Ech hydrogenase. Ech hydrogenase amounts to about 3% of the total cell protein in acetate-grown, methanol-grown or H2/CO2-grown cells of M. barkeri, as calculated from quantitative Western blot experiments. The function of Ech hydrogenase is ascribed to ferredoxin-linked H2 production coupled to the oxidation of the carbonyl-group of acetyl-CoA to CO2 during growth on acetate, and to ferredoxin-linked H2 uptake coupled to the reduction of CO2 to the redox state of CO during growth on H2/CO2 or methanol.     

Patterns of growth and beta-galactosidase production by bifidobacteria

We investigated the patterns of growth and beta-galactosidase formation in the strains Bifidobacterium adolescentis GO-13, MS-42, 91-BIM, and 94-BIM, and B. bifidum No. 1, LVA-3, 791 on media with various carbon sources. The synthesis of beta-galactosidase was shown to be associated with exponential growth of the cultures involved. The maximum specific rate of beta-galactosidase synthesis of 0.20 U mg(-1) h(-1) was observed in B. bifidum LVA-3 after 3-6 h of cultivation. This value for B. adolescentis 91-BIM and 94-BIM was lower and amounted to 0.03-0.08 U mg(-1) h(-1). On the medium with lactose, the highest specific growth rates for B. bifidum LVA-3 and B. bifidum No.1 were 0.38 and 0.60 h(-1), respectively, after 3-6 h of cultivation. For B. adolescentis 91-BIM and 94-BIM, this parameter peaked at 12-15 h of cultivation at 0.13 and 0.22 h(-1), respectively. The hydrolytic activity of beta-galactosidase in the growth medium decreased during the stationary growth phase of the tested cultures.     

Activity and stability of a recombinant plasmid-borne TCE degradative pathway in suspended cultures

The retention and expression of the plasmid-borne, TCE degradative toluene-ortho-monooxygenase (TOM) pathway in suspended continuous cultures of transconjugant Burkholderia cepacia 17616 (TOM31c) were studied. Acetate growth and TCE degradation kinetics for the transconjugant host are described and utilized in a plasmid loss model. Plasmid maintenance did not have a significant effect on the growth rate of the transconjugant. Both plasmid-bearing and plasmid-free strains followed Andrews inhibition growth kinetics when grown on acetate and had maximum growth rates of 0.22 h-1. The transconjugant was capable of degrading TCE at a maximum rate of 9.7 nmol TCE/min. mg protein, which is comparable to the rates found for the original plasmid host, Burkholderia cepacia PR131 (TOM31c). The specific activity of the TOM pathway was found to be a linear function of growth rate. Plasmid maintenance was studied at three different growth rates: 0.17/h, 0.1/h, and 0.065/h. Plasmid maintenance was found to be a function of growth rate, with the probability of loss ranging from 0.027 at a growth rate of 0.065/h to 0.034 at a growth rate 0.17/h.     

Continuous growth kinetics of Candida utilis in pineapple cannery effluent

Candida utilis was grown on a pineapple cannery effluent as the sole carbon and energy source in a chemostat at dilution rates between 0.10 and 0.62 h(-1) to determine the growth kinetics. The principal sugars in the effluent were sucrose, glucose, and fructose. The cell yield coefficient on carbohydrate varied with dilution rate and a maximum value of 0.63 was observed at a dilution rate of 0.33 h(-1). The steady-state concentrations of carbohydrate, reducing sugar, and chemical oxygen demand (COD) appeared to follow Monod saturation kinetics with increasing dilution rate, although none of the measured parameters represented a pure substrate. The maximum specific growth rate and reducing sugar saturation constant were 0.64 h(-1) and 0.060 g/L, respectively. A maximum cell mass productivity of 2.3 g/L h was observed at a dilution rate of 0.51 h(-1). At this dilution rate, only 68% of the COD was removed. A 95% COD removal was attained at a dilution rate of 0.10 h(-1). Optimal yeast productivity and COD reduction occurred at a dilution rate of 0.33 h(-1).